US20050092101A1 - Flanged vortex flowmeter with unitary tapered expanders - Google Patents

Flanged vortex flowmeter with unitary tapered expanders Download PDF

Info

Publication number
US20050092101A1
US20050092101A1 US10/700,263 US70026303A US2005092101A1 US 20050092101 A1 US20050092101 A1 US 20050092101A1 US 70026303 A US70026303 A US 70026303A US 2005092101 A1 US2005092101 A1 US 2005092101A1
Authority
US
United States
Prior art keywords
flowtube
unitary
flanges
vortex
expanders
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
US10/700,263
Other versions
US7082840B2 (en
Inventor
Darroll Bengtson
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Micro Motion Inc
Original Assignee
Rosemount Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Rosemount Inc filed Critical Rosemount Inc
Priority to US10/700,263 priority Critical patent/US7082840B2/en
Assigned to ROSEMOUNT INC. reassignment ROSEMOUNT INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: BENGTSON, DARROLL D.
Priority to JP2004319337A priority patent/JP5346423B2/en
Priority to DE102004053142.0A priority patent/DE102004053142B4/en
Priority to CNB2004100901131A priority patent/CN100397046C/en
Publication of US20050092101A1 publication Critical patent/US20050092101A1/en
Application granted granted Critical
Publication of US7082840B2 publication Critical patent/US7082840B2/en
Assigned to MICRO MOTION, INC. reassignment MICRO MOTION, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ROSEMOUNT INC.
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01FMEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F1/00Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow
    • G01F1/05Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects
    • G01F1/20Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects by detection of dynamic effects of the flow
    • G01F1/32Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects by detection of dynamic effects of the flow using swirl flowmeters
    • G01F1/3209Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects by detection of dynamic effects of the flow using swirl flowmeters using Karman vortices

Definitions

  • This invention relates to flanged vortex flow meters.
  • this invention relates to connecting a vortex flowmeter to a flanged piping system that has a diameter that is larger than a diameter of the vortex flowmeter bore.
  • Vortex flowmeters are used in the industrial process control field for measuring a flow rate of a fluid. Vortex flowmeters are typically inserted in a flow pipe or conduit that carries the fluid to be measured. Industry applications include petroleum, chemical, pulp and paper, mining and materials, oil and gas.
  • the operating principal of a vortex flowmeter is based on a phenomenon of vortex shedding known as the von Karman effect. As fluid passes a bluff body, it separates and generates small eddies or vortices that are shed alternately along and behind each side of the bluff body. These vortices cause areas of fluctuating pressure that are detected by a sensor. While the frequency of vortex generation is essentially proportional to fluid velocity, this proportionality varies with the conduit Reynolds number.
  • the conduit Reynolds number is a function of the fluid density, the fluid viscosity, the fluid velocity, and the inside diameter of the conduit.
  • a manufacturing procedure of a vortex flowmeter allows for assembly of a vortex sensor assembly with one of two or more unitary flowtubes that have bores size numbers that are smaller than flowtube flange size numbers in two or more size number steps.
  • the unitary flowtubes include flanges, flowtube bores and expanders that provide a smooth flow transition from the larger flanges to the smaller bores that is free of joints between the flowtube bore and the expanders.
  • the unitary flowtubes are formed as a single unitary casting.
  • a flow conditioner is cast in an upstream flange of the unitary flowtube.
  • FIG. 1 illustrates a table of size numbers of pipes and vortex flowmeters.
  • FIG. 2 illustrates a graph of power loss in piping systems as a function of flow rate.
  • FIG. 3 illustrates a table of combinations of size numbers for flanges and size numbers for vortex sensor assemblies.
  • FIGS. 4A, 4B illustrate unitary flowtubes that have flowtube flanges of size numbers (N+1), (N+2) and bores of size number N.
  • FIGS. 5A, 5B illustrate unitary flowtubes that are cast as a single unitary bodies.
  • FIGS. 6A, 6B illustrate unitary flowtubes that have flowtube flanges of size number M and bores having size numbers (M ⁇ 1), (M ⁇ 2).
  • FIG. 7 illustrates a vortex flowmeter that includes a flow conditioner.
  • FIG. 8 illustrates an enlarged view of a portion of a flow conditioner.
  • FIG. 9A illustrates a cross-section along line 9 - 9 ′ in FIG. 8 of a flow conditioner that is formed from a thin plate.
  • FIG. 9B illustrates a cross-section along line 9 - 9 ′ in FIG. 8 of a flow conditioner that is formed as a series of vanes.
  • FIG. 10 illustrates an exploded view of a vortex sensor assembly and a standard sensor interface on a unitary flowtube.
  • a manufacturing procedure for a vortex flowmeter allows for assembly of a vortex sensor assembly with one of two or more unitary flowtubes that have bores that are smaller than the flowtube flanges in two or more size number steps.
  • the unitary flowtubes include flanges, flowtube bores and expanders (also called reducers) that provide a smooth flow transition from the larger flanges to the smaller bores.
  • the methods disclosed allow for many combinations of bore size numbers and flange size numbers to be assembled to obtain a desired flow range while having only a single type of vortex sensor with a standard sensor interface in inventory.
  • the flow from a flanged piping system connected to the vortex flowmeter is increased in velocity as it passes through the smaller bore.
  • This arrangement effectively shifts the fluid flow into the measurement range of the vortex flowmeter so that the flow can be measured accurately.
  • the pipe diameter is two standard sizes larger than the flowmeter bore, it is very important to manage the internal surfaces as well as the flow, since the Reynolds number through the flowmeter may be substantially higher locally.
  • the unitary flowtubes are formed as a unitary component so there are no seams between the flowtube bore and the expanders that could cause flow disturbances and inaccuracies.
  • some embodiments include flow conditioners to mitigate the effects of any flow asymmetries since asymmetries are magnified as they pass through the smaller bore. With the disclosed arrangements, the energy savings of using larger flanged pipe in the piping system are achieved along with an accurate flow measurement.
  • FIG. 1 illustrates a table 20 of size numbers of flanged pipes and of vortex flowmeters.
  • piping systems are designed using nominal pipe sizes such as ⁇ fraction (1/2) ⁇ inch, 1 inch, 11 ⁇ 2 inch and so forth.
  • these sequentially increasing nominal pipe sizes are designated by a sequentially increasing size number (N, M, etc.) for convenience in describing embodiments of the invention.
  • Examples of typical vortex flowmeter measurement ranges are shown in FIG. 1 in gallons per minute (GPM) for a vortex flowmeter that has a bore with the nominal diameter indicated in the table in FIG. 1 .
  • GPM gallons per minute
  • the actual inside diameter of a vortex flowmeter bore may be slightly smaller than the actual inside diameter of a flanged pipe of the same nominal inside diameter.
  • the actual inside diameters of flanged pipes are specified by ASME Standards B36.10, ASME B36.19 and ISO Standards ISO 4200, ISO 1127. As can be seen from the example in FIG. 1 , the flow ranges of the vortex flowmeters are limited and also overlap one another.
  • Vortex flowmeters are designed for installation in flanged piping systems that include different pressure ranges and a range of sizes in standardized steps of nominal pipe diameters such as 1 ⁇ 2′′, 3 ⁇ 4′′, 1′′, 11 ⁇ 2′′, 2′′ and larger sizes. Vortex flowmeters are manufactured with flowmeter flanges adapted to mate with pipe flanges of these standardized steps, and with nominal diameters that correspond with the nominal pipe diameters.
  • Vortex flowmeters are usually installed between pipes with a minimum of 10 straight pipe diameters upstream and 5 straight pipe diameters downstream from the vortex flowmeter to reduce the effects of flow disturbances on accuracy. For some types of flow disturbances, up to 35 diameters upstream may be needed to assure accuracy.
  • FIG. 2 illustrates a graph of relative power loss in piping systems as a function of flow rate.
  • a vertical axis 30 represents relative power loss in a piping system in which a vortex flowmeter is used. The power loss is shown only on a relative scale and actual power loss calculations can be scaled based on the composition of the fluid, its temperature and other factors.
  • a horizontal axis 32 represents flow rate in gallons per minute (GPM). The vertical and horizontal axes 30 , 32 have logarithmic scales.
  • Generally diagonal lines 34 , 36 , 38 , 40 , 42 , 44 represent the relative power loss as a function of volumetric flow rate for piping systems of nominal diameters 1, 11 ⁇ 2, 2, 3, 4 and 6 inches, respectively.
  • the flow ranges of vortex flowmeters are shown as rectangular boxes 50 , 52 , 54 , 56 , 58 , 60 , 62 corresponding to nominal sizes of vortex flowmeter bores having nominal diameters 1 ⁇ 2, 1, 11 ⁇ 2, 2, 3, 4 and 6 inches, respectively.
  • FIG. 3 illustrates an example of a table or matrix of combinations of size numbers for flanges and size numbers for bores of vortex unitary flowtubes.
  • the “size numbers” are explained above in connection with FIG. 1 .
  • each of the combinations that is provided in a manufacturing process is marked with an X, and combinations that are not provided are not marked.
  • unitary flowmeters having bores with size number 6 are provided with flanges with size numbers 7 and 8.
  • flowmeters with 4 inch bores are provided with 6 inch and 8 inch flanges.
  • flowmeters having bores with size number N are provided with flanges with size numbers (N+1) and (N+2).
  • unitary flowmeters having flanges with size number 6 are provided with bores with size numbers 4 and 5. Stated another way, flowmeters with 4 inch flanges are provided with 2 and 3 inch bores. Stated in a more general way, flowmeters having flanges with size number M are provided with bores with size numbers (M ⁇ 2) and (M ⁇ 1). These combinations are explained in more detail below in connection with an example illustrated in FIGS. 6A, 6B .
  • Each of the combinations provided as indicated by an X in FIG. 3 includes a standard vortex sensor interface on the unitary flowtube.
  • This arrangement allows finished manufacture of the vortex flowmeter to be completed by simply assembling one of the unitary flowtube combinations with a vortex sensor assembly that is shaped to fit the standard sensor interface.
  • the vortex flowtubes are calibrated using measured flow rates with the reducers and flanges in place. Then the calibrations are stored in the finished vortex flowmeter, preferably in an EEPROM included in the vortex flowmeter electronics. Any accuracy variation due to the expanders is corrected in the calibration process.
  • the right combination of a desired flow range and a flowmeter flange that matches the size of the flanges of the piping system can be accurately, quickly and economically manufactured and shipped. There is no delay in waiting for a vortex flowmeter to be custom manufactured.
  • FIGS. 4A, 4B illustrate unitary flowtubes 80 , 82 that have flowtube flanges of size numbers (N+1), (N+2) and bores of size number N.
  • the two unitary flowtubes 80 , 82 have bores with the same size number N and have the same selected flow measurement range as one another, such as the flow measurement range associated with the size number N in the examples shown in FIG. 1 .
  • a manufacturing method for vortex flowmeter includes providing vortex sensor assemblies shaped to fit a standard sensor interface 86 on each of the unitary flowtube 80 , 82 .
  • the first unitary flowtube 80 is provided and has the standard sensor interface 86 , flowtube flanges 88 of size number (N+1) coupled by tapered expanders 90 to a first bore 92 of size number N.
  • the first unitary flowtube 80 provides a first flange size number (N+1) that is oversized by one step for the selected measurement range.
  • the second unitary flowtube 82 is provided and has the standard sensor interface 86 , flowtube flanges 98 of size number (N+2) coupled by tapered expanders 100 to a second bore 102 of size number N.
  • the second unitary flowtube 82 provides a second flange size number (N+2) that is oversized by two steps for the selected measurement range.
  • a vortex flowmeter with flanges having a selected size number N+1 or N+2 is selected and joined to one vortex sensor assembly at the standard sensor interface 86 on the selected one of the first and second unitary flowtubes 80 , 82 .
  • the expanders 90 , 100 are preferably formed together with pipe flanges 88 , 98 as a single seamless casting that is machined to final shape including weld necks 94 , 104 .
  • the flowmeter bores 92 , 102 are also machined to include weld necks 96 , 106 .
  • the rims of the weld necks on the expanders 90 , 100 are precisely aligned and joined by welding to the facing rims of the weld necks 96 , 106 on the flowmeter bores 92 , 102 .
  • the completed welds are carefully inspected and machined as needed to provide a completely smooth inside diameter for the unitary flowtube that is free of any misalignments or protrusions that could adversely affect the accuracy of the flow measurement.
  • the completed unitary flowtubes 80 , 82 are unitary, in other words, completely free of protruding joints where the expanders are welded to the bores. Because the joints are permanently welded, there is no danger of accidental disassembly and misalignment upon re-assembly at a customer location.
  • FIGS. 5A, 5B illustrate unitary flowtubes 130 , 132 that are cast as single unitary bodies.
  • the unitary flowtubes 130 , 132 of FIGS. 5A, 5B are similar to the unitary flowtubes 80 , 82 of FIGS. 4A, 4B .
  • Reference numbers used in FIGS. 5A, 5B that are the same as reference numbers used in FIGS. 4A, 4B identify the same or similar features.
  • the unitary flowtubes 130 , 132 are each cast as a single unitary casting and machined to final shape, thereby avoiding any seams or gaskets between the bore and the expanders that could disturb flow and adversely affect accuracy.
  • the unitary flowtubes of FIGS. 5A, 5B are similar to the corresponding unitary flowtubes in FIGS. 4A, 4B .
  • FIGS. 4A, 4B , 5 A, 5 B correspond generally with the example 70 illustrated in FIG. 3 .
  • FIGS. 6A, 6B illustrate unitary flowtubes 150 , 152 that have flowtube flanges 162 , 164 of size number M and bores having size numbers (M ⁇ 1) at 92 , (M ⁇ 2) at 102 .
  • the two unitary flowtubes 150 , 152 have flanges with same size number M and have different selected flow measurement ranges, such as those associated with the size numbers M ⁇ 1, M ⁇ 2 in the example table shown in FIG. 1 .
  • the unitary flowtubes illustrated in FIGS. 6A, 6B are similar to the unitary flowtubes illustrated in FIGS. 5A, 5B and reference numbers used in FIGS. 6A, 6B that are the same as reference numbers used in FIGS. 5A, 5B identify the same or similar features.
  • a manufacturing method for vortex flowmeters includes providing vortex sensor assemblies shaped to fit a standard sensor interface 156 , 158 on each of the unitary flowtube 150 , 152 .
  • the first unitary flowtube 150 having the standard sensor interface 156 is provided.
  • the unitary flowtube 150 has flowtube flanges 162 of size number M coupled by tapered expanders 90 to a first bore 92 of size number (M ⁇ 1 ) to provide a first flow measurement range.
  • the second unitary flowtube 152 having the standard sensor interface 158 is provided.
  • the unitary flowtube 152 has flowtube flanges 164 of size number M coupled by tapered expanders 100 to a second bore 102 of size number (M ⁇ 2 ) to provide a second flow measurement range.
  • unitary flowtubes 150 , 152 is similar to the construction of the unitary flowtubes 130 , 132 .
  • the unitary flowtubes 150 , 152 are made from a single casting, but can also be welded as described above in connection with FIGS. 4A, 4B .
  • the examples illustrated in FIGS. 6A, 6B correspond with the example 72 illustrated in FIG. 3 .
  • FIGS. 4A, 4B or FIGS. 5A, 5B are examples of a single bore size number with multiple flange size numbers according to example 70 in FIG. 3 .
  • the examples illustrated in FIGS. 6A, 6B are examples of multiple bore size numbers with a single flange size number according to example 72 in FIG. 3 .
  • FIG. 7 illustrates a vortex flowmeter 176 with a unitary flowtube 178 (such as described above in connection with FIGS. 4A, 4B , 5 A, 5 B, 6 A, 6 B) that includes a flow conditioner 180 .
  • the vortex flowmeter 176 includes a vortex sensor assembly 174 that is mounted to a top flat surface of the unitary flowtube 178 by four bolts (not illustrated).
  • the vortex sensor assembly 174 includes a standard sensor interface that is described in more detail below in connection with FIG. 10 .
  • the flow conditioner 180 is arranged to fit in an inside diameter 182 of an upstream or inlet flange 184 on unitary flowtube 178 .
  • the flow conditioner is larger than a diameter of a bore 186 of the unitary flowtube 178 .
  • a vortex shedding bar 188 is secured in the bore 186 .
  • the flow conditioner 180 includes multiple holes 190 which allow fluid to flow through the flow conditioner.
  • the flow conditioner 180 also includes a solid portion 192 surrounding the holes 190 and blocking fluid flow.
  • the flow conditioner 180 is described in more detail below in connection with FIGS. 8, 9A , 9 B.
  • Vortex flowmeter electronics 194 are provided in a transmitter housing 196 that can be locally mounted as shown, or remotely mounted.
  • the vortex flowmeter electronics preferably includes an electrically erasable read only programmable memory (EEPROM) 198 that stores the calibration data that is obtained by testing the flowtube 184 in a flow test facility.
  • EEPROM electrically erasable read only programmable memory
  • Holes 190 are illustrated in FIG. 7 , it will be understood that the shape of the holes can vary depending on the needs of the application. Holes 190 can be oval or long slots.
  • FIG. 8 illustrates an enlarged broken away view of a portion of a flow conditioner 200 .
  • the flow conditioner 200 includes holes 202 , 204 with edges 206 , 208 that are not sharp, but are instead smoothed or streamlined to reduce turbulence and better condition the flow.
  • the flow conditioner 200 straightens flow so that the flow tends to enter the unitary flowtube relatively free of large vortices that could otherwise disturb measurement accuracy.
  • FIG. 9A illustrates a cross-section along line 9 - 9 ′ in FIG. 8 of a flow conditioner that is formed from a thin plate.
  • the flow conditioner comprises a plate perforated by multiple holes 202 , 204 .
  • the plate has streamlined edges 206 , 208 around the multiple holes 202 , 204 .
  • FIG. 9B illustrates a cross-section along line 9 - 9 ′ in FIG. 8 of a flow conditioner that is formed as a series of streamlined vanes 210 in a plate that is thicker than the plate illustrated in FIG. 9A .
  • FIG. 10 illustrates a fragmentary exploded view of a unitary flowtube bore 220 and a vortex sensor assembly 222 .
  • Flowmeter bore 220 is surrounded by a spool shaped cross section 224 that joins with reducers as explained above in connection with FIGS. 4A, 4B .
  • the spool 224 can be welded to the reducers at weld neck flanges or integrally cast with the reducers.
  • the spool has an inner diameter 226 of size number N which defines the bore 220 . Fluid flows through the bore 220 in a direction indicated by an arrow 228 .
  • a vortex shedding bar 230 extends transversely across the bore 220 and is secured at both ends to the inner diameter surface of the spool 224 .
  • a small flexure section includes a thin sensing diaphragm 232 which is supported along peripheral portions by the vortex shedding bar 230 .
  • the sensing diaphragm 232 is open to the fluid for deflecting laterally in the direction of arrows 234 in response to the alternating forces applied by vortices shed by the vortex shedding bar 230 .
  • a beam 236 is coupled to the sensing diaphragm 232 for transferring deflection of sensing diaphragm 232 through the spool 224 .
  • the beam 236 rotates or “rocks” about a pivot axis 238 in response to deflection of the sensing diaphragm 232 , thereby applying a lateral force on the piezoelectric vortex sensor assembly 222 attached to spool 224 .
  • Piezoelectric vortex sensor assembly 222 senses the lateral movement of the beam 236 and generates a piezoelectric sensor signal on an electrical output 240 having a frequency that is representative of the frequency of vortex shedding and thus the flow rate of the fluid flowing through bore 220 .
  • the electrical output 240 is connected to vortex flowmeter electronics.
  • the vortex sensor assembly 222 is shaped to fit in a hole 242 in a top flat surface of the spool 224 and engage the beam 236 .
  • the size and shape of the hole 242 and the beam 236 are a standardized sensor interface on the unitary flowtube.
  • the arrangement shown in FIG. 10 can be as taught in U.S. Pat. No. 4,926,695 Kleven et al., which is hereby incorporated by reference.

Abstract

A manufacturing procedure of a vortex flowmeter is disclosed that allows for assembly of a vortex sensor assembly with one of two or more unitary flowtubes that have bores that are smaller than the flowtube flanges in two or more size number steps. The unitary flowtubes include flanges, flowtube bores and expanders (also called reducers) that provide a smooth flow transition from the larger flanges to the smaller bores.

Description

    FIELD OF THE INVENTION
  • This invention relates to flanged vortex flow meters. In particular, this invention relates to connecting a vortex flowmeter to a flanged piping system that has a diameter that is larger than a diameter of the vortex flowmeter bore.
  • BACKGROUND OF THE INVENTION
  • Vortex flowmeters are used in the industrial process control field for measuring a flow rate of a fluid. Vortex flowmeters are typically inserted in a flow pipe or conduit that carries the fluid to be measured. Industry applications include petroleum, chemical, pulp and paper, mining and materials, oil and gas. The operating principal of a vortex flowmeter is based on a phenomenon of vortex shedding known as the von Karman effect. As fluid passes a bluff body, it separates and generates small eddies or vortices that are shed alternately along and behind each side of the bluff body. These vortices cause areas of fluctuating pressure that are detected by a sensor. While the frequency of vortex generation is essentially proportional to fluid velocity, this proportionality varies with the conduit Reynolds number. The conduit Reynolds number is a function of the fluid density, the fluid viscosity, the fluid velocity, and the inside diameter of the conduit.
  • In piping systems, there is a desire to keep the Reynolds number low in order to reduce power loss in the piping system. This desire to reduce power loss leads to use of larger pipe sizes and lower ranges of fluid flow velocity in the piping system.
  • In vortex flowmeters, there are limits to the range of flows that are measurable. When flow velocities are below a lower limit of measurable flow, the vortex flowmeter cannot be relied upon to provide an accurate indication of flow.
  • There is a need to provide a vortex flowmeter with an accurate flow output over a range of flows found in piping systems where a larger pipe size is used to reduce power loss.
  • SUMMARY OF THE INVENTION
  • A manufacturing procedure of a vortex flowmeter is disclosed that allows for assembly of a vortex sensor assembly with one of two or more unitary flowtubes that have bores size numbers that are smaller than flowtube flange size numbers in two or more size number steps. The unitary flowtubes include flanges, flowtube bores and expanders that provide a smooth flow transition from the larger flanges to the smaller bores that is free of joints between the flowtube bore and the expanders.
  • In one preferred arrangement, the unitary flowtubes are formed as a single unitary casting. In another preferred arrangement, a flow conditioner is cast in an upstream flange of the unitary flowtube.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 illustrates a table of size numbers of pipes and vortex flowmeters.
  • FIG. 2 illustrates a graph of power loss in piping systems as a function of flow rate.
  • FIG. 3 illustrates a table of combinations of size numbers for flanges and size numbers for vortex sensor assemblies.
  • FIGS. 4A, 4B illustrate unitary flowtubes that have flowtube flanges of size numbers (N+1), (N+2) and bores of size number N.
  • FIGS. 5A, 5B illustrate unitary flowtubes that are cast as a single unitary bodies.
  • FIGS. 6A, 6B illustrate unitary flowtubes that have flowtube flanges of size number M and bores having size numbers (M−1), (M−2).
  • FIG. 7 illustrates a vortex flowmeter that includes a flow conditioner.
  • FIG. 8 illustrates an enlarged view of a portion of a flow conditioner.
  • FIG. 9A illustrates a cross-section along line 9-9′ in FIG. 8 of a flow conditioner that is formed from a thin plate.
  • FIG. 9B illustrates a cross-section along line 9-9′ in FIG. 8 of a flow conditioner that is formed as a series of vanes.
  • FIG. 10 illustrates an exploded view of a vortex sensor assembly and a standard sensor interface on a unitary flowtube.
  • DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • A manufacturing procedure for a vortex flowmeter is disclosed that allows for assembly of a vortex sensor assembly with one of two or more unitary flowtubes that have bores that are smaller than the flowtube flanges in two or more size number steps. The unitary flowtubes include flanges, flowtube bores and expanders (also called reducers) that provide a smooth flow transition from the larger flanges to the smaller bores. The methods disclosed allow for many combinations of bore size numbers and flange size numbers to be assembled to obtain a desired flow range while having only a single type of vortex sensor with a standard sensor interface in inventory.
  • The flow from a flanged piping system connected to the vortex flowmeter is increased in velocity as it passes through the smaller bore. This arrangement effectively shifts the fluid flow into the measurement range of the vortex flowmeter so that the flow can be measured accurately. In embodiments where the pipe diameter is two standard sizes larger than the flowmeter bore, it is very important to manage the internal surfaces as well as the flow, since the Reynolds number through the flowmeter may be substantially higher locally. The unitary flowtubes are formed as a unitary component so there are no seams between the flowtube bore and the expanders that could cause flow disturbances and inaccuracies. Additionally, some embodiments include flow conditioners to mitigate the effects of any flow asymmetries since asymmetries are magnified as they pass through the smaller bore. With the disclosed arrangements, the energy savings of using larger flanged pipe in the piping system are achieved along with an accurate flow measurement.
  • Although it is possible to generate flow vortices in a vortex flowmeter with Reynolds numbers in the range of 2000-10,000, the frequency of the vortices at these low flow rates is not predictably linear. Generally, a Reynolds number of 20,000 is a lower limit for linear flow measurement. An additional lower limit on vortex meter operation is found in the minimum velocity that can be detected by the sensors in the vortex flowmeters. There are different detection limits depending on whether the fluid is a liquid or a gas, and in particular detection depends on fluid density and velocity.
  • FIG. 1 illustrates a table 20 of size numbers of flanged pipes and of vortex flowmeters. As can be seen in FIG. 1, piping systems are designed using nominal pipe sizes such as {fraction (1/2)} inch, 1 inch, 1½ inch and so forth. In this application, these sequentially increasing nominal pipe sizes are designated by a sequentially increasing size number (N, M, etc.) for convenience in describing embodiments of the invention. Examples of typical vortex flowmeter measurement ranges are shown in FIG. 1 in gallons per minute (GPM) for a vortex flowmeter that has a bore with the nominal diameter indicated in the table in FIG. 1. It will be understood by those skilled in the art that the actual inside diameter of a vortex flowmeter bore may be slightly smaller than the actual inside diameter of a flanged pipe of the same nominal inside diameter. The actual inside diameters of flanged pipes are specified by ASME Standards B36.10, ASME B36.19 and ISO Standards ISO 4200, ISO 1127. As can be seen from the example in FIG. 1, the flow ranges of the vortex flowmeters are limited and also overlap one another.
  • Vortex flowmeters are designed for installation in flanged piping systems that include different pressure ranges and a range of sizes in standardized steps of nominal pipe diameters such as ½″, ¾″, 1″, 1½″, 2″ and larger sizes. Vortex flowmeters are manufactured with flowmeter flanges adapted to mate with pipe flanges of these standardized steps, and with nominal diameters that correspond with the nominal pipe diameters.
  • The accuracy of vortex flowmeters is sensitive to flow disturbances. For example, if gasket material between flanges extends into the flow stream, the gasket can disturb the flow and cause inaccurate measurements. Vortex flowmeters are usually installed between pipes with a minimum of 10 straight pipe diameters upstream and 5 straight pipe diameters downstream from the vortex flowmeter to reduce the effects of flow disturbances on accuracy. For some types of flow disturbances, up to 35 diameters upstream may be needed to assure accuracy.
  • In the design of process piping systems, it is common practice to “oversize” piping to reduce flow velocities and thereby reduce the high energy costs of pumping fluid through the process piping system. With the oversize piping, flow rates can easily drop below the linear range of a vortex flowmeter with the same nominal diameter as the pipes. The vortex flowmeter cannot measure the low end of the flow range while also utilizing the upper range capability of the vortex flowmeter since the upper range capability is beyond the upper range of pipe flow. When this situation occurs, it is necessary to provide an “undersized” vortex flow meter that is undersized by one pipe size step and use pipe reducers to connect the undersized vortex flowmeter to the large sized pipes. In many cases, this will increase the flow velocity in the vortex flowmeter enough to measure the lower pipe flow velocities, without incurring an unacceptable increase in energy costs due to the pressure drop across the vortex flowmeter.
  • FIG. 2 illustrates a graph of relative power loss in piping systems as a function of flow rate. A vertical axis 30 represents relative power loss in a piping system in which a vortex flowmeter is used. The power loss is shown only on a relative scale and actual power loss calculations can be scaled based on the composition of the fluid, its temperature and other factors. A horizontal axis 32 represents flow rate in gallons per minute (GPM). The vertical and horizontal axes 30, 32 have logarithmic scales. Generally diagonal lines 34, 36, 38, 40, 42, 44 represent the relative power loss as a function of volumetric flow rate for piping systems of nominal diameters 1, 1½, 2, 3, 4 and 6 inches, respectively. For a given desired flow measurement range 48 of about 3-10 gallons per minute, it can be seen that the relative power loss in the piping system decreases as the nominal pipe size increases. To take advantage of this decrease in power loss, a relatively large size pipe such as a 4 inch pipe can be selected as indicated by the solid line 42.
  • The flow ranges of vortex flowmeters are shown as rectangular boxes 50, 52, 54, 56, 58, 60, 62 corresponding to nominal sizes of vortex flowmeter bores having nominal diameters ½, 1, 1½, 2, 3, 4 and 6 inches, respectively. By comparing the flow range 60 of a 4 inch bore flowmeter with the desired measurement range 48, it can be seen that the flow range 60 covers only a small upper portion of the desired flow range 48. It can also be seen that a 2 inch flowmeter or a 1½ inch flowmeter will cover the entire desired flow measurement range 48. In other words, in this particular example, the piping system has a size number N=6 (4″ diameter with power loss curve 42) and the bore of vortex flowmeters that will accurately measure the desired flow range 48 are size number N=4 (at 56) and N=3 (at 54). The size number N=2 also covers the measurement range, but would result in excessive power loss because of its small size. If a smaller size flanged vortex flowmeter were connected to the larger piping system using conventional flanged reducers and gaskets, the arrangement would be at risk of deviating substantially from the factory calibration of the vortex flowmeter due to the irregularities of mating of the multiple flanges and the protrusion of portions of gaskets into the flowstream. The installation costs of providing two flanged reducers and assembling four flanged pipe connections is very high. This problem is overcome, as explained below in connection with FIGS. 3-10 by providing a unitary flowtube that does not have flanged connections or gaskets between the bore of the flowmeter and the reducers.
  • FIG. 3 illustrates an example of a table or matrix of combinations of size numbers for flanges and size numbers for bores of vortex unitary flowtubes. The “size numbers” are explained above in connection with FIG. 1. In this particular example, each of the combinations that is provided in a manufacturing process is marked with an X, and combinations that are not provided are not marked.
  • For example, as illustrated at 70, unitary flowmeters having bores with size number 6 are provided with flanges with size numbers 7 and 8. Stated another way, flowmeters with 4 inch bores are provided with 6 inch and 8 inch flanges. Stated in a more general way, flowmeters having bores with size number N are provided with flanges with size numbers (N+1) and (N+2). These combinations are explained in more detail below in connection with FIGS. 4A, 4B, 5A, 5B.
  • In another example, as illustrated at 72, unitary flowmeters having flanges with size number 6 are provided with bores with size numbers 4 and 5. Stated another way, flowmeters with 4 inch flanges are provided with 2 and 3 inch bores. Stated in a more general way, flowmeters having flanges with size number M are provided with bores with size numbers (M−2) and (M−1). These combinations are explained in more detail below in connection with an example illustrated in FIGS. 6A, 6B.
  • Each of the combinations provided as indicated by an X in FIG. 3 includes a standard vortex sensor interface on the unitary flowtube. This arrangement allows finished manufacture of the vortex flowmeter to be completed by simply assembling one of the unitary flowtube combinations with a vortex sensor assembly that is shaped to fit the standard sensor interface. The vortex flowtubes are calibrated using measured flow rates with the reducers and flanges in place. Then the calibrations are stored in the finished vortex flowmeter, preferably in an EEPROM included in the vortex flowmeter electronics. Any accuracy variation due to the expanders is corrected in the calibration process. In terms of the needs of a customer, the right combination of a desired flow range and a flowmeter flange that matches the size of the flanges of the piping system can be accurately, quickly and economically manufactured and shipped. There is no delay in waiting for a vortex flowmeter to be custom manufactured.
  • FIGS. 4A, 4B illustrate unitary flowtubes 80, 82 that have flowtube flanges of size numbers (N+1), (N+2) and bores of size number N. The two unitary flowtubes 80, 82 have bores with the same size number N and have the same selected flow measurement range as one another, such as the flow measurement range associated with the size number N in the examples shown in FIG. 1.
  • A manufacturing method for vortex flowmeter includes providing vortex sensor assemblies shaped to fit a standard sensor interface 86 on each of the unitary flowtube 80, 82.
  • The first unitary flowtube 80 is provided and has the standard sensor interface 86, flowtube flanges 88 of size number (N+1) coupled by tapered expanders 90 to a first bore 92 of size number N. The first unitary flowtube 80 provides a first flange size number (N+1) that is oversized by one step for the selected measurement range.
  • The second unitary flowtube 82 is provided and has the standard sensor interface 86, flowtube flanges 98 of size number (N+2) coupled by tapered expanders 100 to a second bore 102 of size number N. The second unitary flowtube 82 provides a second flange size number (N+2) that is oversized by two steps for the selected measurement range.
  • Finally, a vortex flowmeter with flanges having a selected size number N+1 or N+2 is selected and joined to one vortex sensor assembly at the standard sensor interface 86 on the selected one of the first and second unitary flowtubes 80, 82.
  • The expanders 90, 100 are preferably formed together with pipe flanges 88, 98 as a single seamless casting that is machined to final shape including weld necks 94, 104. The flowmeter bores 92, 102 are also machined to include weld necks 96, 106. The rims of the weld necks on the expanders 90, 100 are precisely aligned and joined by welding to the facing rims of the weld necks 96, 106 on the flowmeter bores 92, 102. The completed welds are carefully inspected and machined as needed to provide a completely smooth inside diameter for the unitary flowtube that is free of any misalignments or protrusions that could adversely affect the accuracy of the flow measurement. The completed unitary flowtubes 80, 82 are unitary, in other words, completely free of protruding joints where the expanders are welded to the bores. Because the joints are permanently welded, there is no danger of accidental disassembly and misalignment upon re-assembly at a customer location.
  • FIGS. 5A, 5B illustrate unitary flowtubes 130, 132 that are cast as single unitary bodies. The unitary flowtubes 130, 132 of FIGS. 5A, 5B are similar to the unitary flowtubes 80, 82 of FIGS. 4A, 4B. Reference numbers used in FIGS. 5A, 5B that are the same as reference numbers used in FIGS. 4A, 4B identify the same or similar features. The unitary flowtubes 130, 132 are each cast as a single unitary casting and machined to final shape, thereby avoiding any seams or gaskets between the bore and the expanders that could disturb flow and adversely affect accuracy. In other respects, the unitary flowtubes of FIGS. 5A, 5B are similar to the corresponding unitary flowtubes in FIGS. 4A, 4B.
  • The examples illustrated in FIGS. 4A, 4B, 5A, 5B correspond generally with the example 70 illustrated in FIG. 3.
  • FIGS. 6A, 6B illustrate unitary flowtubes 150, 152 that have flowtube flanges 162, 164 of size number M and bores having size numbers (M−1) at 92, (M−2) at 102. The two unitary flowtubes 150, 152 have flanges with same size number M and have different selected flow measurement ranges, such as those associated with the size numbers M−1, M−2 in the example table shown in FIG. 1. The unitary flowtubes illustrated in FIGS. 6A, 6B are similar to the unitary flowtubes illustrated in FIGS. 5A, 5B and reference numbers used in FIGS. 6A, 6B that are the same as reference numbers used in FIGS. 5A, 5B identify the same or similar features.
  • A manufacturing method for vortex flowmeters includes providing vortex sensor assemblies shaped to fit a standard sensor interface 156, 158 on each of the unitary flowtube 150, 152.
  • The first unitary flowtube 150 having the standard sensor interface 156 is provided. The unitary flowtube 150 has flowtube flanges 162 of size number M coupled by tapered expanders 90 to a first bore 92 of size number (M−1) to provide a first flow measurement range.
  • The second unitary flowtube 152 having the standard sensor interface 158 is provided. The unitary flowtube 152 has flowtube flanges 164 of size number M coupled by tapered expanders 100 to a second bore 102 of size number (M−2) to provide a second flow measurement range.
  • In other respects, the construction of unitary flowtubes 150, 152 is similar to the construction of the unitary flowtubes 130, 132. The unitary flowtubes 150, 152 are made from a single casting, but can also be welded as described above in connection with FIGS. 4A, 4B. The examples illustrated in FIGS. 6A, 6B correspond with the example 72 illustrated in FIG. 3.
  • The examples illustrated in FIGS. 4A, 4B or FIGS. 5A, 5B are examples of a single bore size number with multiple flange size numbers according to example 70 in FIG. 3. The examples illustrated in FIGS. 6A, 6B are examples of multiple bore size numbers with a single flange size number according to example 72 in FIG. 3.
  • FIG. 7 illustrates a vortex flowmeter 176 with a unitary flowtube 178 (such as described above in connection with FIGS. 4A, 4B, 5A, 5B, 6A, 6B) that includes a flow conditioner 180. The vortex flowmeter 176 includes a vortex sensor assembly 174 that is mounted to a top flat surface of the unitary flowtube 178 by four bolts (not illustrated). The vortex sensor assembly 174 includes a standard sensor interface that is described in more detail below in connection with FIG. 10.
  • The flow conditioner 180 is arranged to fit in an inside diameter 182 of an upstream or inlet flange 184 on unitary flowtube 178. The flow conditioner is larger than a diameter of a bore 186 of the unitary flowtube 178. A vortex shedding bar 188 is secured in the bore 186. The flow conditioner 180 includes multiple holes 190 which allow fluid to flow through the flow conditioner. The flow conditioner 180 also includes a solid portion 192 surrounding the holes 190 and blocking fluid flow. The flow conditioner 180 is described in more detail below in connection with FIGS. 8, 9A, 9B.
  • Vortex flowmeter electronics 194 are provided in a transmitter housing 196 that can be locally mounted as shown, or remotely mounted. The vortex flowmeter electronics preferably includes an electrically erasable read only programmable memory (EEPROM) 198 that stores the calibration data that is obtained by testing the flowtube 184 in a flow test facility.
  • While round holes 190 are illustrated in FIG. 7, it will be understood that the shape of the holes can vary depending on the needs of the application. Holes 190 can be oval or long slots.
  • FIG. 8 illustrates an enlarged broken away view of a portion of a flow conditioner 200. The flow conditioner 200 includes holes 202, 204 with edges 206, 208 that are not sharp, but are instead smoothed or streamlined to reduce turbulence and better condition the flow. The flow conditioner 200 straightens flow so that the flow tends to enter the unitary flowtube relatively free of large vortices that could otherwise disturb measurement accuracy.
  • FIG. 9A illustrates a cross-section along line 9-9′ in FIG. 8 of a flow conditioner that is formed from a thin plate. The flow conditioner comprises a plate perforated by multiple holes 202, 204. The plate has streamlined edges 206, 208 around the multiple holes 202, 204.
  • FIG. 9B illustrates a cross-section along line 9-9′ in FIG. 8 of a flow conditioner that is formed as a series of streamlined vanes 210 in a plate that is thicker than the plate illustrated in FIG. 9A.
  • FIG. 10 illustrates a fragmentary exploded view of a unitary flowtube bore 220 and a vortex sensor assembly 222. Flowmeter bore 220 is surrounded by a spool shaped cross section 224 that joins with reducers as explained above in connection with FIGS. 4A, 4B. The spool 224 can be welded to the reducers at weld neck flanges or integrally cast with the reducers. The spool has an inner diameter 226 of size number N which defines the bore 220. Fluid flows through the bore 220 in a direction indicated by an arrow 228.
  • A vortex shedding bar 230 extends transversely across the bore 220 and is secured at both ends to the inner diameter surface of the spool 224. A small flexure section includes a thin sensing diaphragm 232 which is supported along peripheral portions by the vortex shedding bar 230. The sensing diaphragm 232 is open to the fluid for deflecting laterally in the direction of arrows 234 in response to the alternating forces applied by vortices shed by the vortex shedding bar 230. A beam 236 is coupled to the sensing diaphragm 232 for transferring deflection of sensing diaphragm 232 through the spool 224. The beam 236 rotates or “rocks” about a pivot axis 238 in response to deflection of the sensing diaphragm 232, thereby applying a lateral force on the piezoelectric vortex sensor assembly 222 attached to spool 224. Piezoelectric vortex sensor assembly 222 senses the lateral movement of the beam 236 and generates a piezoelectric sensor signal on an electrical output 240 having a frequency that is representative of the frequency of vortex shedding and thus the flow rate of the fluid flowing through bore 220. The electrical output 240 is connected to vortex flowmeter electronics. The vortex sensor assembly 222 is shaped to fit in a hole 242 in a top flat surface of the spool 224 and engage the beam 236. The size and shape of the hole 242 and the beam 236 are a standardized sensor interface on the unitary flowtube. The arrangement shown in FIG. 10 can be as taught in U.S. Pat. No. 4,926,695 Kleven et al., which is hereby incorporated by reference.
  • Although the present invention has been described with reference to preferred embodiments, workers skilled in the art will recognize that changes may be made in form and detail without departing from the scope of the invention.

Claims (19)

1. A manufacturing method for a vortex flowmeter, comprising:
providing unitary flowtubes with larger upstream and downstream flanges, smaller flowtube bores and expanders that provide smooth transitioning from the larger upstream and downstream flanges to the smaller bores; and
providing a flow conditioner in each unitary flowtube that is formed with the upstream flange as a single unitary casting.
2. The method of claim 1, further comprising:
forming the flowtube flanges, the flow conditioner, the expanders, and the bores of each unitary flowtube as a single unitary casting; and
machining the single unitary castings to provide the smooth transitioning.
3. the method of claim 1, further comprising:
measuring a calibration of each unitary flowtube with the flow conditioners, expanders and flanges in place; and
storing the measured calibration in the vortex flowmeter.
4. The method of claim 1, further comprising:
providing weld neck flanges on facing rims of the expanders and the bores;
welding the weld neck flanges together to join the expanders to the bores with smooth weld joints.
5. A method for finishing manufacture of a vortex flowmeter with a bore of size number N for installation between pipe flanges ranging from size number (N+1) to size number (N+2), comprising:
A. providing vortex sensor assemblies shaped to fit a standard sensor interface on a unitary flowtube;
B. providing a first unitary flowtube having the standard sensor interface, upstream and downstream flowtube flanges of size number (N+1) coupled by tapered expanders to a first bore of size number N to provide a first flange size number;
C. providing a second unitary flowtube having the standard sensor interface, upstream and downstream flowtube flanges of size number (N+2) coupled by tapered expanders to a second bore of size number N to provide a second flange size number; and
D. assembling a vortex flowmeter with upstream and downstream flanges having a selected size number by joining one vortex sensor assembly to the standard interface on a selected one of the first and second unitary flowtubes.
6. the method of claim 5, further comprising:
measuring a calibration of each vortex flowtube with the expanders and flanges in place; and
storing the measured calibrations in the vortex flowmeter.
7. A method for finishing manufacture of a vortex flowmeter with a selectable measurement range for installation between pipe flanges of size number N, comprising:
A. providing vortex sensor assemblies shaped to fit a standard sensor interface on a unitary flowtube;
B. providing a first unitary flowtube having the standard sensor interface, upstream and downstream flowtube flanges of size number M coupled by tapered expanders to a first bore of size number (M−1) to provide a first flow measurement range, the upstream flange;
C. providing a second unitary flowtube having the standard sensor interface, upstream and downstream flowtube flanges of size number M coupled by tapered expanders to a second bore of size number (M−2) to provide a second flow measurement range, the upstream flange; and
D. assembling a vortex flowmeter with a selected measurement range by joining one vortex sensor assembly to the standard interface on a selected one of the first and second unitary flowtubes.
8. The method of claim 7, further comprising:
providing weld neck flanges on the expanders and the first and second bores;
welding the weld neck flanges together to join the expanders to the first and second bores with seamless joints.
9. the method of claim 7, further comprising:
measuring the calibration of each vortex flowtube with the expanders and flanges in place; and
storing the measured calibrations in the vortex flowmeters.
10. A vortex flowmeter for installation between pipe flanges of size N, comprising:
A. a vortex sensor assembly shaped to fit a standard sensor interface on a unitary flowtube;
B. a unitary flowtube having the standard sensor interface and having upstream and downstream flowtube flanges of size N, and a bore of size number (N-A) where A is an integer in the range 1, 2 and having expanders coupling between the flowtube flanges and the bore; and
C. the unitary flowtube being formed as a unitary casting that is free of seams.
11. The vortex flowmeter of claim 10 further comprising a flow conditioner that comprises a plate perforated by multiple holes that is part of the unitary casting.
12. The vortex flowmeter of claim 11 wherein the plate has streamlined edges around the multiple holes.
13. The vortex flowmeter of claim 10 wherein the flow conditioner comprises vanes having streamlined edges.
14. the vortex flowmeter of claim 10, further comprising:
a measured calibration with the expanders, and flanges in place stored in the vortex flowmeter.
15. A vortex flowmeter for installation between pipe flanges of size N, comprising:
A. a vortex sensor assembly shaped to fit a standard sensor interface on a unitary flowtube;
B. a unitary flowtube having the standard sensor interface and having upstream and downstream flowtube flanges of size N, and a bore of a size number at least as small as (N−1), and having expanders coupling between the flowtube flanges and the bore; and
C. a flow conditioner of size number N across an opening in the upstream flange.
16. The vortex flowmeter of claim 15 wherein the flow conditioner comprises a plate perforated by multiple holes.
17. The vortex flowmeter of claim 16 wherein the plate has streamlined edges around the multiple holes.
18. The vortex flowmeter of claim 15 wherein the flow conditioner comprises vanes having streamlined edges.
19. the vortex flowmeter of claim 15, further comprising:
a measured calibration with the expander, flanges and flow conditioner in place stored in the vortex flowmeter.
US10/700,263 2003-11-03 2003-11-03 Flanged vortex flowmeter with unitary tapered expanders Expired - Lifetime US7082840B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
US10/700,263 US7082840B2 (en) 2003-11-03 2003-11-03 Flanged vortex flowmeter with unitary tapered expanders
JP2004319337A JP5346423B2 (en) 2003-11-03 2004-11-02 Flanged vortex flowmeter with integral taper diameter expansion
DE102004053142.0A DE102004053142B4 (en) 2003-11-03 2004-11-03 Flanged vortex flowmeter with unitary tapered extension pieces
CNB2004100901131A CN100397046C (en) 2003-11-03 2004-11-03 Flanged vortex flowmeter with unitary tapered expanders

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US10/700,263 US7082840B2 (en) 2003-11-03 2003-11-03 Flanged vortex flowmeter with unitary tapered expanders

Publications (2)

Publication Number Publication Date
US20050092101A1 true US20050092101A1 (en) 2005-05-05
US7082840B2 US7082840B2 (en) 2006-08-01

Family

ID=34551179

Family Applications (1)

Application Number Title Priority Date Filing Date
US10/700,263 Expired - Lifetime US7082840B2 (en) 2003-11-03 2003-11-03 Flanged vortex flowmeter with unitary tapered expanders

Country Status (4)

Country Link
US (1) US7082840B2 (en)
JP (1) JP5346423B2 (en)
CN (1) CN100397046C (en)
DE (1) DE102004053142B4 (en)

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070163361A1 (en) * 2006-01-19 2007-07-19 Lewicke Joseph J Reduced bore vortex flowmeter having a stepped intake
US20070277733A1 (en) * 2006-06-05 2007-12-06 Wood Thomas L Apparatus for applying a protective layer to a pipe joint
US20080072686A1 (en) * 2006-07-21 2008-03-27 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
DE102006047815A1 (en) * 2006-10-06 2008-04-10 Endress + Hauser Flowtec Ag Measuring system e.g. magnetic-inductive flow measuring system, for detecting measurement variable e.g. mass flow of medium, has flow conditioner with inner edge that is provided upstream of outlet end of conditioner and projects into lumen
DE102007030691A1 (en) 2007-06-30 2009-01-02 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
DE102007030699A1 (en) 2007-06-30 2009-01-15 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
DE102007037166A1 (en) 2007-08-07 2009-02-19 Endress + Hauser Flowtec Ag gauge
DE102007030690A1 (en) 2007-06-30 2009-05-07 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
DE102007030700A1 (en) 2007-06-30 2009-05-07 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
US20090120206A1 (en) * 2006-04-20 2009-05-14 Naoki Matsubara Explosion-Proof High Temperature Compatible, Multi-Vortex Flow Meter
DE102007063372A1 (en) 2007-12-30 2009-07-02 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
US20090217771A1 (en) * 2007-07-19 2009-09-03 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
DE102009002289A1 (en) 2009-04-08 2010-10-14 Endress + Hauser Flowtec Ag Method for determining period duration of periodic primary signal for determining e.g. mass flow rate, involves generating reference clock signal, and determining period duration based on number and reference values
US20160334249A1 (en) * 2015-05-14 2016-11-17 Daniel Sawchuk Flow Conditioner Having Integral Pressure Tap
US20170254688A1 (en) * 2014-10-21 2017-09-07 Micro Motion, Inc. Apparatus for applying a variable zero algorithm in a vibrating flowmeter and related method
WO2019071342A1 (en) * 2017-10-11 2019-04-18 Romet Limited Rotary gas meter with flange connection
US10365143B2 (en) 2016-09-08 2019-07-30 Canada Pipeline Accessories, Co., Ltd. Measurement ring for fluid flow in a pipeline
US10416009B1 (en) * 2016-02-12 2019-09-17 FlowPro, LLC Vortex shedding flowmeter with wide dynamic range piezoelectric vortex sensor
US10633237B2 (en) * 2010-12-23 2020-04-28 Sidel S.P.A. Con Socio Unico System and method for filling a container with a pourable product
CN113108850A (en) * 2021-05-28 2021-07-13 津制仪表(天津)有限公司 Novel vortex street flowmeter

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7650798B2 (en) * 2007-03-06 2010-01-26 Rosemount Inc. Vented high-temperature piezoelectric-based field device
DE102008017141A1 (en) 2008-04-03 2009-10-29 Siemens Aktiengesellschaft Field device for process instrumentation
US8459127B2 (en) * 2008-10-29 2013-06-11 Rosemount Inc. Flowmeter body with a groove in a flowmeter outlet surface
DE102008060095B3 (en) * 2008-12-02 2010-06-10 Siemens Aktiengesellschaft Field device e.g. pressure transducer, for e.g. process instrumentation in technical process system, has base rings covering flange pressing side such that ends of half rings are provided between head or nut of fastening screws and side
US9032815B2 (en) 2011-10-05 2015-05-19 Saudi Arabian Oil Company Pulsating flow meter having a bluff body and an orifice plate to produce a pulsating flow
US9016138B2 (en) * 2013-03-13 2015-04-28 Rosemount Inc. Flanged reducer vortex flowmeter
US9464926B2 (en) * 2014-09-23 2016-10-11 Micro Motion, Inc. Magnetic flowmeter flowtube assembly with spring-energized seal rings
WO2020208697A1 (en) * 2019-04-09 2020-10-15 株式会社エルフ Flow rate sensor

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4186599A (en) * 1976-12-29 1980-02-05 Rosemount Inc. Vortex shedding flowmeter assembly
US4841781A (en) * 1987-12-04 1989-06-27 Schlumberger Industries, Inc. Flow rectifier for vortex flowmeter
US4926695A (en) * 1987-09-15 1990-05-22 Rosemount Inc. Rocking beam vortex sensor
US5052229A (en) * 1989-05-23 1991-10-01 Mitsubishi Jidosha Kogyo Kabushiki Kaisha Vortex flowmeter
US6053053A (en) * 1998-03-13 2000-04-25 Rosemount Inc. Multiple vortex flowmeter system
US6658945B1 (en) * 1997-03-27 2003-12-09 Rosemount Inc. Vortex flowmeter with measured parameter adjustment

Family Cites Families (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3874234A (en) * 1973-06-27 1975-04-01 Fischer & Porter Co Vortex shedding flowmeter
JPS55101815A (en) * 1979-01-30 1980-08-04 Oval Eng Co Ltd Vortex flowmeter
JPH0711438B2 (en) * 1987-01-22 1995-02-08 日本電装株式会社 Air flowmeter with rectifying grid
US4718283A (en) * 1987-01-30 1988-01-12 Itt Corporation Vortex meter body
JPH0267224U (en) * 1988-11-10 1990-05-22
DE4013351A1 (en) * 1989-04-25 1990-10-31 Mitsubishi Motors Corp Vortex flow meter
ATE118071T1 (en) * 1989-07-20 1995-02-15 Univ Salford Business Services FLOW CONDITIONER.
JP2898835B2 (en) * 1992-12-14 1999-06-02 株式会社オーバル Vortex flow meter
US6003383A (en) * 1994-03-23 1999-12-21 Schlumberger Industries, S.A. Vortex fluid meter incorporating a double obstacle
FR2717897B1 (en) * 1994-03-23 1996-06-07 Schlumberger Ind Sa Vortex fluid meter with a profiled line.
JPH08110252A (en) * 1994-10-13 1996-04-30 Fuji Electric Co Ltd Karman's vortex flowmeter
JPH08247810A (en) * 1995-03-14 1996-09-27 Tokico Ltd Vortex flowmeter and manufacture thereof
JP3430284B2 (en) * 1997-06-17 2003-07-28 横河電機株式会社 Vortex flow meter
JPH11258016A (en) * 1998-03-13 1999-09-24 Yokogawa Electric Corp Vortex flow meter
JPH11344366A (en) * 1998-06-02 1999-12-14 Yokogawa Electric Corp Vortex flowmeter
GB9912561D0 (en) * 1999-05-28 1999-07-28 Fusion Meters Ltd Meter
US6615673B1 (en) * 1999-07-26 2003-09-09 The Foxboro Company Integral shedder and mounting pad
JP3232482B2 (en) * 1999-09-08 2001-11-26 株式会社リガルジョイント Kalman vortex sensor-Manifold holder for capsule-
CN2404103Y (en) * 1999-12-27 2000-11-01 温州市瓯海自动化仪表厂 Cyclone flowmeter
CN2434647Y (en) * 2000-07-19 2001-06-13 北京博思达仪器仪表有限公司 Reducing rectifier for measuring
JP2002048610A (en) * 2000-07-31 2002-02-15 Yokogawa Electric Corp Vortex flowmeter
CN2440201Y (en) * 2000-09-22 2001-07-25 陈宝荣 Intelligent vortex-street flow meter
JP2002139365A (en) * 2000-11-02 2002-05-17 Oval Corp Method and apparatus for mounting flowmeter

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4186599A (en) * 1976-12-29 1980-02-05 Rosemount Inc. Vortex shedding flowmeter assembly
US4926695A (en) * 1987-09-15 1990-05-22 Rosemount Inc. Rocking beam vortex sensor
US4841781A (en) * 1987-12-04 1989-06-27 Schlumberger Industries, Inc. Flow rectifier for vortex flowmeter
US5052229A (en) * 1989-05-23 1991-10-01 Mitsubishi Jidosha Kogyo Kabushiki Kaisha Vortex flowmeter
US6658945B1 (en) * 1997-03-27 2003-12-09 Rosemount Inc. Vortex flowmeter with measured parameter adjustment
US6053053A (en) * 1998-03-13 2000-04-25 Rosemount Inc. Multiple vortex flowmeter system

Cited By (40)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1991837A4 (en) * 2006-01-19 2009-03-11 Invensys Sys Inc Reduced bore vortex flowmeter having a stepped intake
WO2007084629A3 (en) * 2006-01-19 2007-12-27 Invensys Sys Inc Reduced bore vortex flowmeter having a stepped intake
US20070163361A1 (en) * 2006-01-19 2007-07-19 Lewicke Joseph J Reduced bore vortex flowmeter having a stepped intake
US7533579B2 (en) 2006-01-19 2009-05-19 Invensys Systems, Inc. Reduced bore vortex flowmeter having a stepped intake
EP1991837A2 (en) * 2006-01-19 2008-11-19 Invensys Systems, Inc. Reduced bore vortex flowmeter having a stepped intake
US7861602B2 (en) * 2006-04-20 2011-01-04 Oval Corporation Explosion-proof high temperature compatible, multi-vortex flow meter
US20090120206A1 (en) * 2006-04-20 2009-05-14 Naoki Matsubara Explosion-Proof High Temperature Compatible, Multi-Vortex Flow Meter
US20070277733A1 (en) * 2006-06-05 2007-12-06 Wood Thomas L Apparatus for applying a protective layer to a pipe joint
US20100037704A1 (en) * 2006-07-21 2010-02-18 Endress + Hauser Flowtec Ag Measuring system with a flow conditioner arranged at an inlet of a measuring tube
US7603914B2 (en) 2006-07-21 2009-10-20 Endress + Hauser Flowtec Ag Measuring system with a flow conditioner arranged at an inlet of a measuring tube
US20080072686A1 (en) * 2006-07-21 2008-03-27 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
US7926361B2 (en) 2006-07-21 2011-04-19 Endress + Hauser Flowtec Ag Measuring system with a flow conditioner arranged at an inlet of a measuring tube
US20100043566A1 (en) * 2006-07-21 2010-02-25 Endress + Hauser Flowtec Ag Measuring system with a flow conditioner arranged at an inlet of a measuring table
US20080072688A1 (en) * 2006-07-21 2008-03-27 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
US20100011878A1 (en) * 2006-07-21 2010-01-21 Endress + Hauser Flowtec Ag Measuring system with a flow conditioner arranged at an inlet of a measuring tube
US8079271B2 (en) 2006-07-21 2011-12-20 Endress + Hauser Flowtec Ag Measuring system with a flow conditioner arranged at an inlet of a measuring tube
US7946186B2 (en) 2006-07-21 2011-05-24 Endress + Hauser Flowtec Ag Measuring system with a flow conditioner arranged at an inlet of a measuring tube
US7600436B2 (en) 2006-07-21 2009-10-13 Endress + Hauser Flowtec Ag Measuring system with a flow conditioner arranged at an inlet of a measuring tube
US7878073B2 (en) 2006-07-21 2011-02-01 Endress + Hauser Flowtec Ag Measuring system with a flow conditioner arranged at an inlet of a measuring table
DE102006047815A1 (en) * 2006-10-06 2008-04-10 Endress + Hauser Flowtec Ag Measuring system e.g. magnetic-inductive flow measuring system, for detecting measurement variable e.g. mass flow of medium, has flow conditioner with inner edge that is provided upstream of outlet end of conditioner and projects into lumen
DE102007030691A1 (en) 2007-06-30 2009-01-02 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
DE102007030700A1 (en) 2007-06-30 2009-05-07 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
DE102007030690A1 (en) 2007-06-30 2009-05-07 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
DE102007030699A1 (en) 2007-06-30 2009-01-15 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
US20090217771A1 (en) * 2007-07-19 2009-09-03 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
US7882751B2 (en) 2007-07-19 2011-02-08 Endress + Hauser Flowtec Ag Measuring system with a flow conditioner for flow profile stabilization
DE102007037166A1 (en) 2007-08-07 2009-02-19 Endress + Hauser Flowtec Ag gauge
DE102007063372A1 (en) 2007-12-30 2009-07-02 Endress + Hauser Flowtec Ag Measuring system for a medium flowing in a process line
DE102009002289A1 (en) 2009-04-08 2010-10-14 Endress + Hauser Flowtec Ag Method for determining period duration of periodic primary signal for determining e.g. mass flow rate, involves generating reference clock signal, and determining period duration based on number and reference values
US10633237B2 (en) * 2010-12-23 2020-04-28 Sidel S.P.A. Con Socio Unico System and method for filling a container with a pourable product
US20170254688A1 (en) * 2014-10-21 2017-09-07 Micro Motion, Inc. Apparatus for applying a variable zero algorithm in a vibrating flowmeter and related method
US11226221B2 (en) * 2014-10-21 2022-01-18 Micro Motion, Inc. Apparatus for applying a variable zero algorithm in a vibrating flowmeter and related method
US9625293B2 (en) * 2015-05-14 2017-04-18 Daniel Sawchuk Flow conditioner having integral pressure tap
US20160334249A1 (en) * 2015-05-14 2016-11-17 Daniel Sawchuk Flow Conditioner Having Integral Pressure Tap
US10416009B1 (en) * 2016-02-12 2019-09-17 FlowPro, LLC Vortex shedding flowmeter with wide dynamic range piezoelectric vortex sensor
US10365143B2 (en) 2016-09-08 2019-07-30 Canada Pipeline Accessories, Co., Ltd. Measurement ring for fluid flow in a pipeline
US10677632B2 (en) 2016-09-08 2020-06-09 Canada Pipeline Accessories, Co., Ltd. Measurement ring for fluid flow in a pipeline
WO2019071342A1 (en) * 2017-10-11 2019-04-18 Romet Limited Rotary gas meter with flange connection
US11143538B2 (en) 2017-10-11 2021-10-12 Romet Limited Rotary gas meter with flange connection
CN113108850A (en) * 2021-05-28 2021-07-13 津制仪表(天津)有限公司 Novel vortex street flowmeter

Also Published As

Publication number Publication date
DE102004053142A1 (en) 2005-06-02
CN100397046C (en) 2008-06-25
US7082840B2 (en) 2006-08-01
JP2005164581A (en) 2005-06-23
CN1614362A (en) 2005-05-11
JP5346423B2 (en) 2013-11-20
DE102004053142B4 (en) 2017-10-26

Similar Documents

Publication Publication Date Title
US7082840B2 (en) Flanged vortex flowmeter with unitary tapered expanders
US8548753B2 (en) Velocity-enhanced flow measurement
US6053053A (en) Multiple vortex flowmeter system
EP2372315B1 (en) Vortex flow meter with vortex oscillation sensor plate
US9016138B2 (en) Flanged reducer vortex flowmeter
US11255707B2 (en) Hybrid flow meter with vortex sensor and differential pressure sensor arrangements with fluid flow meter diagnostics
EP2444781A1 (en) Ultrasonic measurement of flow velocity
US7533579B2 (en) Reduced bore vortex flowmeter having a stepped intake
US11371866B2 (en) Methods for designing a flow conduit and apparatus that measures deflection at multiple points to determine flow rate
WO2010002432A1 (en) Insertable ultrasonic meter and method
CN105021236B (en) Flow meter
Howe et al. Orifices
Krishna et al. Experimental analysis of multiport averaging device and effect of body shape on flow coefficient
Lomas et al. Application and Selection
US20230194403A1 (en) Volume fraction meter for multiphase fluid flow
AU2011239256B2 (en) Method for Generating a Diagnostic from a Deviation of a Flow Meter Parameter
KR100394345B1 (en) segmental wedge DP flow meter
American Water Works Association Flowmeters in Water Supply: M33
KR20220137349A (en) Ultrasonic Flow Meter
von Lavante et al. Effects of manufacturing tolerances on the accuracy of vortex-shedding flow meters
Hardy Flowmeters for use in the nuclear industry: How to select the appropriate instrument
Hogendoorn et al. Flow disturbances and flow conditioners: The effect on multi-beam ultrasonic flow meters
HOWE et al. 2.15 Orifices
Vaidya DESIGN & DEVELOPMENT OF 16 INCH INLINE VORTEX FLOWMETER WITH NOISE CANCELLATION SENSOR.
LIPTÁK 2.14 Orifices

Legal Events

Date Code Title Description
AS Assignment

Owner name: ROSEMOUNT INC., MINNESOTA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:BENGTSON, DARROLL D.;REEL/FRAME:014666/0245

Effective date: 20031029

STCF Information on status: patent grant

Free format text: PATENTED CASE

FPAY Fee payment

Year of fee payment: 4

FPAY Fee payment

Year of fee payment: 8

AS Assignment

Owner name: MICRO MOTION, INC., COLORADO

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:ROSEMOUNT INC.;REEL/FRAME:038772/0175

Effective date: 20160415

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 12TH YEAR, LARGE ENTITY (ORIGINAL EVENT CODE: M1553)

Year of fee payment: 12